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The PSD and Orifice Discharge in MSMA 2 OSD Calculation

3 min read

For small developments (under 5 hectares), MSMA 2nd Edition provides a simplified calculation for On-Site Detention (OSD), where the design involves using pre-computed tables and figures (Table 5.A1, 5.A2, 5.A3, and 5.A4) to determine the permissible discharge (PSD), required storage volume (SSR) and the size of the inflow and outflow pipes. This method is a quick and easy way to design minor drainage systems specifically for 10-year ARI design storms, where engineers do not have to do detailed calculation and just extract the figures from the tables.

While MSMA guideline provided us with the PSD as a maximum allowable peak outflow, it did not indicate the calculation of orifice discharge using Equation 2.6 in MSMA.

 Q=Av=C_dA\sqrt{2gH_o}

Here, we go through Appendix 5.B (page 5-28), rework the example as per the table method and calculate the actual orifice discharge. We notice that the orifice discharge of the suggested outlet size is way bigger than the PSD obtained in the table. This is somehow inconsistent and questionable.

Result #

Development site

: Negeri Sembilan – Kuala Pilah

Region in MSMA

: Region 1 – West Coast

Catchment area

: 0.61 ha

Terrain type

: Mild

% Impervious area

: 75.0%

Storage dimension (L x W X D)

: 20m x 12m x 1.2m

Site Storage Requirement, SSR

: 273.77 m3

Permissible Site Discharge, PSD

(whichever lesser from 5.A1 and 5.A2)

: 0.028 m3/s

Suggested outlet pipe size from the table

(whichever lesser from 5.A3 and 5.A4)

: 172 mm

Outlet pipe invert level

: At the bottom of the OSD (PIL 1.20)

Effective head, H_0

: 1.1140m

Actual Orifice Discharge

: 0.066 m3/s

Actual Orifice Discharge check with PSD?

: 0.066 m3/s> 0.028 m3/s (Not OK!)

For a given pipe diameter from MSMA table, the outlet discharge > PSD, which is not satisfactory and debatable

Another 5 sites of each region are selected and calculated to observe the PSD and the actual orifice discharge. All of the actual orifice discharge is way higher than the tabulated PSD as per table below.

File sample here

Information

Catchment area : 0.8ha
Terrain type : Mild
% Impervious area : 90%
Outlet pipe position : At the tank bottom

 

Site location

Region

SSR (m3)

Storage dimension

(L x W X D) (m)

Eff head,H0 (m)

PSD (m3/s)

Orifice size from table, D0 (mm)

Orifice Discharge (m3/s)

Orifice discharge with PSD check

Ipoh, Perak

1 – West Coast

403.76

20 x 15 x 1.5

1.4015

0.063

197

0.099

Qout < PSD

(Not OK!)

Kuantan, Pahang

2 – East Coast

542.96

20 x 15 x 2.0

1.9125

0.050

175

0.091

Qout < PSD

(Not OK!)

Alor Setar, Kedah

3 – Northern

417.28

20 x 15 x 1.5

1.4070

0.056

186

0.089

Qout < PSD

(Not OK!)

Cameron Highland, Pahang

4 – Highlands

407.36

-Ditto-

1.4220

0.035

156

0.063

Qout < PSD

(Not OK!)

Batu Pahat, Johor

5 – Southern

425.84

-Ditto-

1.4030

0.046

194

0.096

Qout < PSD

(Not OK!)

Effective head (H0) = Height of storage – [Orifice Elevation from bottom of OSD + D0/2]

 Orifice discharge (Q)=Av=C_dA\sqrt{2gH_o}

How to obtain Effective Head (H_0)

Hypothesis #

In order to achieve outlet discharge to be lesser than the PSD, we need to either set the outlet pipe invert level to be higher, or  reduce the outlet pipe diameter. In this section, we will adjust the effective head and outlet size, to get the orifice discharge similar to the PSD value, and observe the difference.

Adjust pipe invert level (i.e.: adjust effective head) #

The comparison was performed by adjusting the pipe invert level to be higher than the tank base, while keeping the pipe diameter as specified in the table.

Site location

Orifice size from table, D0 (mm)

Eff head, H_0 (m)

Adjusted Eff head,H_0 (m)

Adjusted Pipe Level from storage bed (m)

PSD (m3/s)

Orifice Discharge (m3/s)

Orifice discharge with PSD check

% Difference

(|Adj H0 – H0| / H0)

Ipoh, Perak

197

1.4015

0.5715

0.830

0.063

0.063

OK!

59.22

Kuantan, Pahang

175

1.9125

0.5825

1.330

0.050

0.050

OK!

69.54

Alor Setar, Kedah

186

1.4070

0.5670

0.840

0.056

0.056

OK!

59.70

Cameron Highland, Pahang

156

1.4220

0.4420

0.980

0.035

0.035

OK!

68.92

Batu Pahat, Johor

194

1.4030

0.3130

1.090

0.046

0.046

OK!

77.69

To achieve the same discharge as the PSD, we find that we need to consistently reduce the effective head ( or make the pipe level higher than the storage Invert Level). There seems to be no regularity to how high the pipe level should be adjusted upwards.

Adjust outlet pipe diameter #

The comparison was carried out by adjusting the pipe diameter, while the pipe invert level was kept fixed at the tank bottom.

Site location

Eff head,H_0 (m)

Original Orifice size from table, D_0 (mm)

Adjusted orifice size, D0 (mm)

PSD (m3/s)

Orifice Discharge (m3/s)

Orifice discharge with PSD check

% Difference

(|Adj D0 – D0| / D0)

Ipoh, Perak

1.4215

197

157

0.063

0.063

OK!

20.30

Kuantan, Pahang

1.9350

175

130

0.050

0.050

OK!

25.71

Alor Setar, Kedah

1.4265

186

147

0.056

0.056

OK!

20.97

Cameron Highland, Pahang

1.4225

156

115

0.035

0.035

OK!

26.28

Batu Pahat, Johor

1.4335

194

133

0.046

0.046

OK!

31.44

From the above comparison, to achieve the same discharge as the PSD, we will have to use a smaller orifice size, holding the effective head constant.

Conclusion #

PSD is consistently smaller than the orifice discharge in the sites that we chose for our study, assuming that the orifice is lying on the bottom of the OSD. It is not immediately clear how MSMA designers come up with how many percent the Orifice Discharge has to be reduced to give us the PSD, but it does seem that from our sample calculation, the PSD value is computed by reducing the orifice diameter size to 20% to 30%.

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